US4308288A - Method of producing granular cocoa - Google Patents
Method of producing granular cocoa Download PDFInfo
- Publication number
- US4308288A US4308288A US06/128,508 US12850880A US4308288A US 4308288 A US4308288 A US 4308288A US 12850880 A US12850880 A US 12850880A US 4308288 A US4308288 A US 4308288A
- Authority
- US
- United States
- Prior art keywords
- cocoa
- powder
- cocoa powder
- granules
- agglomerates
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 235000009470 Theobroma cacao Nutrition 0.000 title claims abstract description 121
- 238000000034 method Methods 0.000 title claims description 36
- 244000240602 cacao Species 0.000 title 1
- 244000299461 Theobroma cacao Species 0.000 claims abstract description 127
- 239000000843 powder Substances 0.000 claims abstract description 70
- 239000008187 granular material Substances 0.000 claims abstract description 39
- 230000032683 aging Effects 0.000 claims abstract description 11
- 238000007906 compression Methods 0.000 claims abstract description 5
- 230000006835 compression Effects 0.000 claims abstract description 5
- 239000002245 particle Substances 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 5
- 235000008476 powdered milk Nutrition 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 20
- 235000013336 milk Nutrition 0.000 abstract description 3
- 239000008267 milk Substances 0.000 abstract description 3
- 210000004080 milk Anatomy 0.000 abstract description 3
- 230000000704 physical effect Effects 0.000 abstract description 3
- 239000011230 binding agent Substances 0.000 abstract description 2
- 235000019197 fats Nutrition 0.000 description 8
- YSXLJTGZMRNQSG-UHFFFAOYSA-L disodium;6-amino-5-[[2-[4-[2-[4-[2-[(2-amino-5-sulfonatonaphthalen-1-yl)diazenyl]phenyl]sulfonyloxyphenyl]propan-2-yl]phenoxy]sulfonylphenyl]diazenyl]naphthalene-1-sulfonate Chemical compound [Na+].[Na+].C1=CC=C2C(N=NC3=CC=CC=C3S(=O)(=O)OC3=CC=C(C=C3)C(C)(C=3C=CC(OS(=O)(=O)C=4C(=CC=CC=4)N=NC=4C5=CC=CC(=C5C=CC=4N)S([O-])(=O)=O)=CC=3)C)=C(N)C=CC2=C1S([O-])(=O)=O YSXLJTGZMRNQSG-UHFFFAOYSA-L 0.000 description 5
- 239000000428 dust Substances 0.000 description 5
- 235000019219 chocolate Nutrition 0.000 description 4
- 238000005469 granulation Methods 0.000 description 4
- 230000003179 granulation Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 235000005764 Theobroma cacao ssp. cacao Nutrition 0.000 description 3
- 235000005767 Theobroma cacao ssp. sphaerocarpum Nutrition 0.000 description 3
- 235000001046 cacaotero Nutrition 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 238000005096 rolling process Methods 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- 235000008939 whole milk Nutrition 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 244000046052 Phaseolus vulgaris Species 0.000 description 1
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 1
- IAIWVQXQOWNYOU-BAQGIRSFSA-N [(z)-(5-nitrofuran-2-yl)methylideneamino]urea Chemical compound NC(=O)N\N=C/C1=CC=C([N+]([O-])=O)O1 IAIWVQXQOWNYOU-BAQGIRSFSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229940110456 cocoa butter Drugs 0.000 description 1
- 235000019868 cocoa butter Nutrition 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000005496 tempering Methods 0.000 description 1
- 239000004034 viscosity adjusting agent Substances 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
- A23G1/00—Cocoa; Cocoa products, e.g. chocolate; Substitutes therefor
- A23G1/04—Apparatus specially adapted for manufacture or treatment of cocoa or cocoa products
- A23G1/042—Manufacture or treatment of liquids, creams, pastes, granules, shreds or powders
- A23G1/047—Transformation of liquids, pastes, creams, lumps, powders, granules or shreds into powders, granules or shreds; Manufacture or treatment of powders
Definitions
- This invention relates to a method of producing granular cocoa which is easily soluble in water to give a hot or cold cocoa drink.
- Cocoa powder is obtained fundamentally through the procedures of crushing and winnowing roasted cocoa beans to give so-called cocoa nibs, grinding the nibs to give a slurry called chocolate liquor or cacao mass, passing this slurry through special filter presses to squeeze out extra fat and pulverizing the resulting filtercake, followed by sifting.
- cocoa powder is rather low in fluidity and tends to be suspended in the atmosphere to produce a dust cloud, sometimes threatening to result in a dust explosion.
- cocoa powder is not readily soluble in water and hence offers inconveniences to the consumers.
- To prepare hot cocoa without forming undissolved lumps of cocoa powder it is necessary to take the steps of first pouring a small quantity of hot water on cocoa powder, followed by thorough kneading to obtain a smooth paste, and then adding a larger quantity of hot water and/or hot milk, with enough stirring to achieve satisfactory dispersion and dissolution of the cocoa powder particles.
- cold cocoa drink it is necessary to cool hot cocoa prepared through these steps since it is very difficult to well disperse and dissolve cocoa powder in cold water and/or milk.
- a granulating method wherein cocoa butter and a surfactant are added to and mixed with cacao mass and the paste-like mixture is forced through a wire screen, followed by drying.
- a granular cocoa obtained by this method has a disadvantage that when the granular cocoa is dissolved and dispersed in hot water a large number of glaring oil droplets appear on the surface of the cocoa liquid and give an unpleasant feeling.
- this granulating method needs to comprise a tempering procedure and requires skill.
- granular cocoa is produced through the following steps. First a cocoa powder of which fat content is in the range from 12 to 29% by weight is subjected to such an extent of compression, for example, by means of a compression apparatus of the screw type, that the cocoa powder exhibits an appreciable increase in bulk density but still remains in powder form. Then the cocoa powder in the compressed state is fed to a roller press such that a pair of rolls of the roller press force the individual particles of the cocoa powder to strongly cohere to one another thereby forming small, plate-like and about 0.5-3 mm thick agglomerates of the cocoa powder. These plate-like agglomerates are crushed and sifted to obtain cocoa granules which are between 10 and 30 mesh in size.
- cocoa granules are allowed to age by keeping the cocoa granules at temperatures below about 27° C., and more preferably at 15°-25° C., for a period of about three hours to several days.
- the granulating method according to the invention is applicable not only to pure cocoa powder entirely prepared from cacao mass but also to an adjusted cocoa powder which has been added with sugar, or a substitute sugar, and/or powdered milk.
- the present invention is based on our discovery that fine particles of cocoa powder can be forced to strongly adhere or cohere to one another by initially compressing the powder to a certain extent and then passing the compressed cocoa powder (while in the compressed state) through rolls of a roller press so as to form small and thin plate-like agglomerates. By crushing these agglomerates, followed by sifting, cocoa granules of desired sizes and excellent physical properties can easily be obtained.
- Cocoa powder is low in bulk density, that is, small in weight per unit volume. Therefore, if it is intended to agglomerate cocoa powder to form sufficiently dense and stiff plate-like blocks by passing the powder through rolls with no pre-treatment, the intention can hardly be realized primarily because it is very difficult to feed a sufficient quantity of cocoa powder per unit time to the rolls and, hence, the individual fine particles of the powder are not forced to strongly cohere to one another.
- cocoa powder is first compressed by means of a compressing apparatus such as a screw extruder to such an extent that the powder undergoes an appreciable increase in its weight per unit volume but still remains in powder form. Then, while in the compressed state, the cocoa powder is fed to a roller press and forced to pass through a pair of rolls which are, as usual, arranged parallel and turning in opposite directions.
- a sufficiently large quantity of cocoa powder can be fed to the rolls at a stretch or during each unit time, so that the individual particles of cocoa are well compressed against one another and forced to strongly cohere to one another with the result that thin plate-like agglomerates are formed.
- cocoa powder too low in fat content If use is made of a cocoa powder too low in fat content, forced cohesion of the cocoa powder particles during the agglomerating procedure remains insufficient so that cocoa granules obtained through the succeeding crushing and sifting procedures are insufficient in stiffness and are liable to crumble.
- the use of a cocoa powder too high in fat content is also unfavorable because when the granulated cocoa is dispersed and dissolved in hot water oil droplets appear on the surface of the cocoa liquid and give unpleasant feeling. Therefore, the present invention requires to use a cocoa powder of which fat content is in the range from 12 to 29% by weight.
- the resultant cocoa granules become excessively dense and stiff ones which are inferior in the property of dissolving and dispersing in water.
- the formation of too thick plate-like agglomerates of cocoa powder results in that the coehsion of the cocoa particles remain insufficient and/or occurs non-uniformly and, therefore, that the finally obtained cocoa granules are irregular in hardness and liable to crumble.
- cocoa granules which are between 10 and 30 mesh (ASTM standard sieves) in size. Cocoa granules larger in size are inconvenient to handle with a spoon or the like, but cocoa granules smaller than 30 mesh lose most of the advantages of granular cocoa. In the present invention, therefore, the cocoa granules are made to be between 10 and 30 mesh in size.
- the method of the invention includes an ageing process wherein the granulated cocoa is allowed to age by keeping it at temperatures below about 27° C., and more preferably at 15°-25° C., for a period of a few hours at the shortest and several days at the longest.
- the cocoa granules become sufficiently dense and stiff, meaning that the individual cocoa particles in each grain become quite strongly cohered to one another, and nevertheless the granules become further easily soluble in water.
- the aged cocoa granules have a very desirable color.
- the present invention makes it possible to granulate cocoa powder without the addition of any binder, water or any other auxiliary additive, that is, to obtain a granular cocoa consisting of pure cocoa.
- this invention can provide cocoa granules which do not easily crumble during handling in dry state but are excellent in the property of being dissolved and dispersed in water in spite of the use of no surfactant in the granulating process.
- the dispersion and dissolution property of granular cocoa produced by a method of the invention can be controlled by controlling the thickness of the small plate-like agglomerates of cocoa powder (within the aforementioned range of 0.5-3 mm).
- the granulating method of the invention becomes a solution to the problem of low fluidity of cocoa powder and greatly contributes to the preclusion of dust clouds in cocoa powder plants.
- dissolution of granular cocoa produced according to the invention is not accompanied by the appearance of oil droplets on the surface of the cocoa liquid.
- a roller press was located adjacent the outlet of a screw extruder.
- a pure cocoa powder of which fat content was 22%, was charged into the hopper of the extruder and compressed by the screw.
- the cocoa powder extruded from the screw extruder in a compressed state was directly fed to the roller press such that the rolls forced the compressed powder to become small and 1.2 mm thick plate-like agglomerates.
- These agglomerates were crushed by means of a crusher into smaller granules, which were sifted through sieves to obtain cocoa granules between 16 and 24 mesh.
- These cocoa granules were kept at 21° C. for 48 hr thereby accomplishing ageing.
- the thus produced granular cocoa and a conventional cocoa powder (on the market) containing 22% fat were subjected to a comparative test to examine easiness of dispersing and dissolving each sample in cold or hot water.
- a comparative test to examine easiness of dispersing and dissolving each sample in cold or hot water.
- 5 g of each cocoa sample was poured into water contained in a 200 ml beaker and kept at a predetermined temperature (20° C., 60° C. or 80° C.), and the amount of time elapsed until wetting and submerging of the entire sample was measured, without agitating the water in the beaker.
- the following table presents the result of this test, demonstrating distinct superiority of the granular cocoa (of Example 1) in the dispersing and dissolving property.
- Example 1 Using the extruding and rolling apparatus of Example 1, a pure cocoa powder containing 16% fat was compressed in the screw extruder and directly (in a compressed state) fed to the rolls to form small and 0.8 mm thick plate-like agglomerates of the cocoa powder. These plate-like agglomerates were crushed and sifted to obtain cocoa granules between 22 and 28 mesh. The thus obtained cocoa granules were allowed to age by keeping them in a chamber maintained at 18°-22° C. for 24 hr. As the result, granular cocoa of excellent physical properties was obtained.
- a pure cocoa powder containing 26% fat was treated in accordance with Example 1 to form small and plate-like agglomerates of the cocoa powder which were 1.8-2.0 mm in thickness.
- the plate-like agglomerates were crushed and sifted into cocoa granules 16-24 mesh in size.
- the production of a granular cocoa was completed by ageing these cocoa granules first at 24° C. for 3 hr and thereafter at 16° C. for 24 hr.
- the product of this example too, exhibited excellent properties.
- a chocolate powder was prepared by mixing 36 kg of a pure cocoa powder containing 24% fat and 64 kg of powdered sugar. By the apparatus and procedures of Example 1, this chocolate powder was forced to become small and 1.2 mm thick plate-like agglomerates, which were crushed and sifted into granules between 16 and 24 mesh in size. A granular chocolate of excellent properties was obtained by ageing the granules at 18° C. for 12 hr.
- a drink chocolate powder was prepared by mixing 30 kg of pure cocoa powder containing 24% fat with 70 kg of powdered sugar. This chocolate powder was treated in accordance with Example 4 to obtain granules between 16 and 24 mesh. The production of a granular drink chocolate was completed by keeping the granules at 18° C. for 4 days.
- Example 1 By the apparatus and procedures of Example 1, an instant chocolate powder prepared by mixing 20 kg of pure cocoa powder containing 24% fat, 30 kg of powdered whole milk and 50 kg of powdered sugar was granulated into granules which were between 16 and 24 mesh in size. Through the aging process of Example 1, these granules excellent properties as a granular instant chocolate.
- a cocoa powder mix was prepared by adding 25 kg of powdered whole milk, 57 kg of powdered sugar and small amounts of a flavoring and a viscosity adjusting agent to 18 kg of pure cocoa powder containing 18% fat and subjected to the granulating and aging procedures of Example 1. Obtained as the result was a granular instant cocoa of excellent properties.
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- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Confectionery (AREA)
Abstract
Description
______________________________________
Granular Cocoa
Conventional
Temp. of Water
of Example 1 Cocoa Powder
______________________________________
20° C.
15 sec more than 1 hr*.sup.1
60° C.
0 sec*.sup.2
2 min
80° C.
0 sec*.sup.2
40 sec
______________________________________
*.sup.1 complete submerging did not occur even 1 hr had elapsed: stirred
thereafter, but a portion of the sample still floated on the water
surface.
*.sup.2 dissolved and dispersed instantaneously.
Claims (9)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54158903A JPS604698B2 (en) | 1979-12-07 | 1979-12-07 | Method for producing granulated cocoa |
| JP54-158903 | 1979-12-07 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4308288A true US4308288A (en) | 1981-12-29 |
Family
ID=15681875
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US06/128,508 Expired - Lifetime US4308288A (en) | 1979-12-07 | 1980-03-10 | Method of producing granular cocoa |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US4308288A (en) |
| JP (1) | JPS604698B2 (en) |
Cited By (34)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4713256A (en) * | 1983-08-26 | 1987-12-15 | Clextral | Process for preparing a chocolate paste |
| US4786520A (en) * | 1984-10-19 | 1988-11-22 | Morinaga & Co., Ltd. | Process for manufacturing cocoa |
| US4840809A (en) * | 1988-04-11 | 1989-06-20 | Nestec S.A. | Agglomeration process |
| EP0379023A1 (en) * | 1989-01-16 | 1990-07-25 | Jacobs Suchard AG | Process for making chocolate powder, and this chocolate powder |
| US4954060A (en) * | 1988-04-11 | 1990-09-04 | Nestec S.A. | Apparatus for agglomeration |
| EP0331222A3 (en) * | 1988-03-02 | 1990-12-05 | Unilever Nv | Granular beverage material for tea, coffee or cocoa, and method of its preparation |
| US4980181A (en) * | 1989-01-11 | 1990-12-25 | Nestec S.A. | Chocolate coated beverage mixes |
| US5051269A (en) * | 1985-06-05 | 1991-09-24 | Nestec S.A. | Agglomeration method |
| US5264228A (en) * | 1992-06-01 | 1993-11-23 | Nestec S.A. | Preparation of compositions for making cocoa beverages |
| US5540944A (en) * | 1994-09-30 | 1996-07-30 | Nestec S.A. | Process of preparing a film-coated meat product |
| EP0885567A3 (en) * | 1997-06-20 | 2000-03-22 | Meiji Seika Kaisha Ltd. | Process for producing granular cocoa |
| FR2856244A1 (en) * | 2003-06-20 | 2004-12-24 | Barry Callebaut Ag | CHOCOLATE BEVERAGE PREPARED FROM AN EXPRESSO TYPE MACHINE AND MEANS FOR OBTAINING IT |
| WO2006108592A1 (en) * | 2005-04-15 | 2006-10-19 | Keme Food Engineering Ag | Instant product |
| EP1714557A1 (en) * | 2005-04-20 | 2006-10-25 | Keme Food Engineering AG | Instant product |
| US20070196556A1 (en) * | 2004-07-15 | 2007-08-23 | Van Der Meer Henricus J | Process For The Roasting Of Cocoa |
| US20080193628A1 (en) * | 2005-02-17 | 2008-08-14 | Chiara Garbolino | Process for the Preparation of a Spreadable Dispersion Comprising Sterol |
| US20080220146A1 (en) * | 2007-03-06 | 2008-09-11 | Deboer Rene Frans | Method and apparatus for producing cocoa products |
| WO2009068999A2 (en) | 2007-11-28 | 2009-06-04 | Barry Callebaut Ag | Process and product |
| US20090291176A1 (en) * | 2002-12-02 | 2009-11-26 | Takasago International Corporation | Granulated flavor and method for producing the same |
| US20090291163A1 (en) * | 2008-05-21 | 2009-11-26 | Stokely-Van Camp, Inc. | Milk-based recovery beverage |
| US20100003373A1 (en) * | 2005-04-28 | 2010-01-07 | Meiji Seika Kaisha, Ltd. | Rapidly soluble granules and method for producing the same |
| ITMI20091242A1 (en) * | 2009-07-13 | 2011-01-14 | Lico Spa | PROCEDURE FOR CHOCOLATE PRODUCTION |
| WO2012149261A1 (en) * | 2011-04-28 | 2012-11-01 | The Hershey Company | Cocoa nuggets and method of making same |
| US20130046027A1 (en) * | 2011-08-16 | 2013-02-21 | José Fernando Galdón Miquel | Chocolate with agglomerate structure and the method for preparing thereof |
| US8865245B2 (en) | 2008-12-19 | 2014-10-21 | Conopco, Inc. | Edible fat powders |
| US20150024093A1 (en) * | 2013-07-18 | 2015-01-22 | The Hershey Company | Cocoa and sugar agglomerate for flavored beverages and method of forming same |
| US8940355B2 (en) | 2003-07-17 | 2015-01-27 | Conopco, Inc. | Process for the preparation of an edible dispersion comprising oil and structuring agent |
| US8993035B2 (en) | 2010-12-17 | 2015-03-31 | Conopco, Inc. | Edible water in oil emulsion |
| EP2652123B1 (en) | 2010-12-16 | 2016-01-13 | Merck Patent GmbH | Dry granulated cell culture media |
| US9924730B2 (en) | 2010-06-22 | 2018-03-27 | Unilever Bcs Us, Inc. | Edible fat powders |
| US10219523B2 (en) | 2010-12-17 | 2019-03-05 | Upfield Us Inc. | Process of compacting a microporous fat powder and compacted fat powder so obtained |
| US10226059B2 (en) * | 2013-06-25 | 2019-03-12 | Olam International Limited | Process for producing dark brown natural cocoa |
| WO2021028857A1 (en) * | 2019-08-12 | 2021-02-18 | Industria Colombiana Del Café S. A. S. | Method for obtaining a granulated food material |
| US11324670B2 (en) * | 2013-10-16 | 2022-05-10 | Bilal Walk | Cocoa butter powdered moisturizer |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0258094U (en) * | 1988-10-17 | 1990-04-26 | ||
| JP2004357616A (en) * | 2003-06-06 | 2004-12-24 | Ezaki Glico Co Ltd | Method for treating cocoa powder and method for producing cocoa in which powder is adjusted |
| JP4553635B2 (en) * | 2004-06-03 | 2010-09-29 | 明治製菓株式会社 | Granular cocoa and method for producing the same |
| JP6398031B1 (en) * | 2018-04-10 | 2018-09-26 | 森永製菓株式会社 | Powdered chocolate |
| JP6793269B1 (en) * | 2020-05-08 | 2020-12-02 | 森永製菓株式会社 | Cacao products |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2889225A (en) * | 1955-03-26 | 1959-06-02 | Zora Tovarna Na Cokoladu A Cuk | Method and apparatus for the production of chocolate masses |
| US3053663A (en) * | 1959-11-24 | 1962-09-11 | Corn Products Co | Chocolate drink base and method |
-
1979
- 1979-12-07 JP JP54158903A patent/JPS604698B2/en not_active Expired
-
1980
- 1980-03-10 US US06/128,508 patent/US4308288A/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2889225A (en) * | 1955-03-26 | 1959-06-02 | Zora Tovarna Na Cokoladu A Cuk | Method and apparatus for the production of chocolate masses |
| US3053663A (en) * | 1959-11-24 | 1962-09-11 | Corn Products Co | Chocolate drink base and method |
Cited By (54)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4713256A (en) * | 1983-08-26 | 1987-12-15 | Clextral | Process for preparing a chocolate paste |
| US4786520A (en) * | 1984-10-19 | 1988-11-22 | Morinaga & Co., Ltd. | Process for manufacturing cocoa |
| US5094156A (en) * | 1985-06-05 | 1992-03-10 | Nestec S.A. | Agglomeration apparatus |
| US5051269A (en) * | 1985-06-05 | 1991-09-24 | Nestec S.A. | Agglomeration method |
| EP0331222A3 (en) * | 1988-03-02 | 1990-12-05 | Unilever Nv | Granular beverage material for tea, coffee or cocoa, and method of its preparation |
| AU615410B2 (en) * | 1988-04-11 | 1991-09-26 | Societe Des Produits Nestle S.A. | Apparatus for agglomerating particles |
| AU602843B2 (en) * | 1988-04-11 | 1990-10-25 | Societe Des Produits Nestle S.A. | Agglomeration process |
| US4954060A (en) * | 1988-04-11 | 1990-09-04 | Nestec S.A. | Apparatus for agglomeration |
| US4840809A (en) * | 1988-04-11 | 1989-06-20 | Nestec S.A. | Agglomeration process |
| US4980181A (en) * | 1989-01-11 | 1990-12-25 | Nestec S.A. | Chocolate coated beverage mixes |
| EP0379023A1 (en) * | 1989-01-16 | 1990-07-25 | Jacobs Suchard AG | Process for making chocolate powder, and this chocolate powder |
| US5264228A (en) * | 1992-06-01 | 1993-11-23 | Nestec S.A. | Preparation of compositions for making cocoa beverages |
| US5540944A (en) * | 1994-09-30 | 1996-07-30 | Nestec S.A. | Process of preparing a film-coated meat product |
| US5702741A (en) * | 1994-09-30 | 1997-12-30 | Nestec S.A. | Granular particulate food composition and method of making |
| EP0885567A3 (en) * | 1997-06-20 | 2000-03-22 | Meiji Seika Kaisha Ltd. | Process for producing granular cocoa |
| US20090291176A1 (en) * | 2002-12-02 | 2009-11-26 | Takasago International Corporation | Granulated flavor and method for producing the same |
| FR2856244A1 (en) * | 2003-06-20 | 2004-12-24 | Barry Callebaut Ag | CHOCOLATE BEVERAGE PREPARED FROM AN EXPRESSO TYPE MACHINE AND MEANS FOR OBTAINING IT |
| US11278038B2 (en) | 2003-07-17 | 2022-03-22 | Upfield Europe B.V. | Process for the preparation of an edible dispersion comprising oil and structuring agent |
| US8940355B2 (en) | 2003-07-17 | 2015-01-27 | Conopco, Inc. | Process for the preparation of an edible dispersion comprising oil and structuring agent |
| US20070196556A1 (en) * | 2004-07-15 | 2007-08-23 | Van Der Meer Henricus J | Process For The Roasting Of Cocoa |
| US9661864B2 (en) | 2005-02-17 | 2017-05-30 | Unilever Bcs Us, Inc. | Process for the preparation of a spreadable dispersion |
| US20080317917A1 (en) * | 2005-02-17 | 2008-12-25 | Janssen Johannes Jozef M | Fat Granules |
| US20090136645A1 (en) * | 2005-02-17 | 2009-05-28 | Chiara Garbolino | Granules Comprising Sterol |
| US20080193628A1 (en) * | 2005-02-17 | 2008-08-14 | Chiara Garbolino | Process for the Preparation of a Spreadable Dispersion Comprising Sterol |
| US8124152B2 (en) * | 2005-02-17 | 2012-02-28 | Conopco Inc. | Fat granules |
| US8927045B2 (en) | 2005-02-17 | 2015-01-06 | Sandra Petronella Barendse | Process for the preparation of a spreadable dispersion |
| US20080152779A1 (en) * | 2005-04-15 | 2008-06-26 | Evelyne De Groote | Instant Product |
| WO2006108592A1 (en) * | 2005-04-15 | 2006-10-19 | Keme Food Engineering Ag | Instant product |
| EP1714557A1 (en) * | 2005-04-20 | 2006-10-25 | Keme Food Engineering AG | Instant product |
| US20100003373A1 (en) * | 2005-04-28 | 2010-01-07 | Meiji Seika Kaisha, Ltd. | Rapidly soluble granules and method for producing the same |
| US20080220146A1 (en) * | 2007-03-06 | 2008-09-11 | Deboer Rene Frans | Method and apparatus for producing cocoa products |
| WO2009068999A3 (en) * | 2007-11-28 | 2009-11-05 | Barry Callebaut Ag | Process and product for producing a chocolate or chocolate-like product |
| WO2009068999A2 (en) | 2007-11-28 | 2009-06-04 | Barry Callebaut Ag | Process and product |
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| US8846122B2 (en) | 2007-11-28 | 2014-09-30 | Barry Callebaut Ag | Process and product |
| US20090291163A1 (en) * | 2008-05-21 | 2009-11-26 | Stokely-Van Camp, Inc. | Milk-based recovery beverage |
| US8865245B2 (en) | 2008-12-19 | 2014-10-21 | Conopco, Inc. | Edible fat powders |
| ITMI20091242A1 (en) * | 2009-07-13 | 2011-01-14 | Lico Spa | PROCEDURE FOR CHOCOLATE PRODUCTION |
| WO2011007379A1 (en) * | 2009-07-13 | 2011-01-20 | Lico S.P.A. | "process for the production of chocolate" |
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| US8993035B2 (en) | 2010-12-17 | 2015-03-31 | Conopco, Inc. | Edible water in oil emulsion |
| US8668950B2 (en) | 2011-04-28 | 2014-03-11 | The Hershey Company | Cocoa nuggets and method of making same |
| CN103635095A (en) * | 2011-04-28 | 2014-03-12 | 赫尔希公司 | Cocoa nuggets and method of making same |
| WO2012149261A1 (en) * | 2011-04-28 | 2012-11-01 | The Hershey Company | Cocoa nuggets and method of making same |
| US8790737B2 (en) * | 2011-08-16 | 2014-07-29 | Natra Cacao, S.L. Unipersonal | Chocolate with agglomerate structure and the method for preparing thereof |
| US20130046027A1 (en) * | 2011-08-16 | 2013-02-21 | José Fernando Galdón Miquel | Chocolate with agglomerate structure and the method for preparing thereof |
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| US9017750B2 (en) * | 2013-07-18 | 2015-04-28 | The Hershey Company | Cocoa and sugar agglomerate for flavored beverages and method of forming same |
| US20150024093A1 (en) * | 2013-07-18 | 2015-01-22 | The Hershey Company | Cocoa and sugar agglomerate for flavored beverages and method of forming same |
| US11324670B2 (en) * | 2013-10-16 | 2022-05-10 | Bilal Walk | Cocoa butter powdered moisturizer |
| WO2021028857A1 (en) * | 2019-08-12 | 2021-02-18 | Industria Colombiana Del Café S. A. S. | Method for obtaining a granulated food material |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5682056A (en) | 1981-07-04 |
| JPS604698B2 (en) | 1985-02-06 |
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